Page 210 - International safety guide for oil tankers and terminals
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INTERNATIONAL SAFETY GUIDE FOR OIL TANKERS AND TERMINALS



                                          significant because the ship and terminal are connected by a
                                          common stream of vapours, thereby introducing into the operation
      ---ใช้เพื่อการศึกษาเท่านั้น---
                                          a number of additional hazards which have to be effectively
                                          controlled.

                             11.1.13.3สมุด ศูนย์ฝกพาณิชย์นาวี
                                          Detailed guidance on technical issues associated with vapour
                                          emission control and treatment systems is available from a
                                          number of sources. IMO has developed international standards
                                          for the design, construction and operation of vapour collection
                                          systems on tankers and vapour emission control systems at
                                          terminals, and OCIMF has initiated and issued guidance on
                                          vapour manifold arrangements (see Bibliography).

                                          It should be noted that Vapour Emission Control Systems (VECS)
                                          can serve tankers fitted with inert gas systems and also
                                          non-inerted tankers.

                                          A summary of the terminal’s VECS should be included in the
                                          terminal information booklet.

                             11.1.13.2    Misconnection of Liquid and Vapour Lines

                                          To guard against the possible misconnection of the ship’s vapour
                                          manifold to a terminal liquid loading line, the vapour connection
                                                                          ึ
                                          should be clearly identified by painting the outboard 1 metre
                                          section with yellow and red bands and by stencilling the word
                                          ‘VAPOUR’ in black letters upon it.

                                          In addition, a cylindrical stud should be permanently attached to
                                          each presentation flange face at the 12 o’clock position on the
                                          flange bolt circle. The stud should project 25.4 mm (1 inch)
                                                                                              1
                                          perpendicular to the flange face, and should be 12.7 mm ( ⁄2 inch)
                                          in diameter, in order to prevent the connection of standard liquid
                                          transfer hoses. Blank flanges, inboard ends of reducers and
                                          hoses for the vapour line will have an extra hole to accommodate
                                          the stud on the presentation flange (see Figure 11.3).

                                          Full details of vapour manifold arrangements, materials and
                                          fittings are contained in the OCIMF publication ‘Recommendations
               งานห้อง                    Although all ‘closed’ cargo operations require in-tank pressures to
                                          for Oil Tanker Manifolds and Associated Equipment’.

                                          Vapour Over/Under-Pressure


                                          be effectively monitored and controlled, the connection to a
                                          vapour emission control system results in pressures within the
                                          ship’s vapour spaces being directly influenced by any changes
                                          that may occur within the terminal’s system. It is therefore
                                          important to ensure that the individual cargo tank
                                          pressure/vacuum protection devices are fully operational and that
                                          loading rates do not exceed maximum allowable rates. In addition,
                                          pressures within vapour collection piping systems should be
                                          continuously monitored by sensors that incorporate high and low
                                          pressure alarm functions connected to audible and visual alarms.


                             11.1.13.4    Cargo Tank Overfill
                                          The risk of overfilling a cargo tank when using a VEC system is
                                          no different from that when loading under normal closed




      176                                      © ICS/OCIMF/IAPH 2006
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